Detailed Project Report on oleoresin extraction plant from chillis

OLEORESIN EXTRACTION PLANT FROM CHILLIS [CODE NO.3665]

Oleoresins are the concentrated liquid form of the spice. They are obtained from spices by extraction with a non-aqueous solvent followed by removal of the solvent by evaporation. This spice derivative has the same character and property of the spice it is obtained from. They reproduce the character of the respective spice and spice oil fully. Spice oleoresins represent the complete flavour profile of the spice. It contains the volatile as well as nonvolatile constituents of spices. Oleoresins can replace whole/ground spices without impairing any flavour and aroma characteristic. Spice oleoresins guarantee superior quality of flavour and aroma. They are complete and balanced, consistent, and standardised. The quality of an oleoresin is typically evaluated on the basis of presence of the active ingredients in desired levels. As these are concentrated extracts, they are typically used as a diluted dispersion plated on a neutral dry carrier or as a diluted blend in a solubilizing medium such as vegetable oil to match the desired strength of the ground spice/herb. All the spices contain essential oils in varying proportions which can be extracted by steam distillation.

The main products in a spice oleoresin plant are oleoresins of chilli, pepper, ginger and turmeric. The co-products are corresponding spice oils, which are widely used in food and pharmaceutical industries. Spent meals of spice powders after oleoresin extraction are by-products and are devoid of essential oils, pungent principles, fixed oils and resinous matter for which the spices are valued. This may be considered for incorporation in animal feed formulations, as spent meal is rich in carbohydrate and cellulose.


COST ESTIMATION

Plant Capacity            28480 Ltr/Year      
Land & Building      Rs. 1.57 Cr         
Plant & Machinery                      Rs. 3.02 Cr     
Working Capital for 1 Month     Rs. 1.27 Cr
Total Capital Investment              Rs. 6.44 Cr
Rate of Return            39%                   
Break Even Point             46%                

     
INTRODUCTION    

WHY OLEORESINS?    

TECHNOLOGY    

ADVANTAGES & DISADVANTAGE OF OLEORESINS    

THE ADVANTAGES OF OLEORESINS    

ADVANTAGES & DISADVANTAGE    

ADVANTAGES OF SCFE    

ADVANTAGE OF CO2 AS A SOLVENT    

RAW MATERIALS    

BOTANICAL DESCRIPTION    

NUTRITIONAL VALUE OF CHILLI    

USES    

INDIAN NAME OF SPICES    

FOREIGN NAME OF SPICES    

INDIAN CHILLI VARIETIES    

DIFFERENT VARIETIES    

BIRDS EYE CHILLI (DHANI)    

BYADAGI (KADDI)    

ELLACHIPUR SANNAM-S4 TYPE    

GUNTUR SANNAM-S4 TYPE    

HINDPUR-S7    

JWALA    

KANTHARI-WHITE    

KASHMIR CHILLI    

MADHYA PRADESH G.T.SANNAM    

METHODS OF OLEORESIN EXTRACTION    

SOLVENT EXTRACTION PROCESS    

SUPERCRITICAL FLUID EXTRACTION PROCESS    

STEAM DISTILLATION PROCESS    

SCF MANUFACTURING PROCESS    

SAMPLE PREPARATION    

SUPERCRITICAL FLUID EXTRACTION (SFE)    

SCF TECHNOLOGY DEVEN SUPERCRITICALS PVT. LTD., INDIA    

SPECIAL FEATURES ON OUR SCFE SYSTEM    

PLC BASED CONTROL SYSTEM    

INSTRUMENTATION    

PROPERTIES OF SCF    

PHASE DIAGRAM    

COMPARISON OF SUPERCRITICAL CO2 FLUID EXTRACTION (SCFE)
    AND CHEMICAL EXTRACTION    

SFE ADVANTGE OVER OTHER PROCESS    

SUPERCRITICAL FLUID EXTRACTION TECHNOLOGY AND ITS APPLICATION
    IN FOOD INDUSTRY    

PRINCIPLE AND INFLUENCING FACTORS    

THE BASIC PRINCIPLE OF SUPERCRITICAL FLUID EXTRACTION    

FACTORS INFLUENCING SUPERCRITICAL FLUID EXTRACTION    

RAW MATERIALS    

SOLUBILITY (TEMPERATURE AND PRESSURE)    

APPLICATION STATUS AND PROGRESS    

PROPERTIES OF OLEORESIN    

PHYSICAL PROPERTIES TO BE CHECKED    

EFFECT OF PH STABILITY OF NATURAL OLEORESIN EXTRACTED
   BY SUPERCRITICAL CO2    

HEAT STABILITY OF OLEORESIN EXTRACTED BY SUPERCRITICAL CO2    

TEM OF OLEORESIN NANOPARTICLES EXTRACTED BY SUPERCRITICAL CO2    

TEM OF OLEORESIN NANOPARTICLES EXTRACTED BY SUPERCRITICAL CO2    

STANDARD CURVE OF OLEORESIN    

FT-IR ANALYSIS OF OLEORESIN    

PH STABILITY OF NATURAL OLEORESIN EXTRACTED BY SUPERCRITICAL CO2    

HEAT STABILITY OF OLEORESIN EXTRACTED BY SUPERCRITICAL CO2    

DSC OF NANO OLEORESIN    

VARIOUS OLEORESINS & THEIR APPLICATIONS    

SOLVENTS    

MARKET POTENTIAL    

SPICE OILS AND OLEORESINS MARKET SEGMENTATION    

INDIA DOMINATES GLOBAL MARKET FOR SPICE OLEORESIN AS DEMAND
   FOR NATURAL AGENTS’ SWELLS    

SEGMENTATION    

KEY PLAYERS    

REGIONAL MARKET SUMMARY    

GLOBAL OLEORESINS MARKET SHARE (%), BY REGION, 2017    

GLOBAL OLEORESINS MARKET, BY PRODUCT    

GLOBAL OLEORESINS MARKET, BY RAW MATERIAL    

GLOBAL OLEORESINS MARKET, BY APPLICATION    

GLOBAL OLEORESINS MARKET, BY REGION    

"RISING DEMAND FOR PACKAGED SPICES AND SEASONING IN RESTAURANTS"    

"PAPRIKA OLEORESIN HELD OVER ONE THIRD OF THE REVENUE SHARE IN 2015"    

"FLAVOR WAS THE LARGEST APPLICATION SEGMENT IN 2015"    

"EUROPE HELD OVER ONE-THIRD OF REVENUE SHARE IN 2015"    

"FEW COMPANIES HOLD A LARGE MARKET SHARE OF THE OVERALL OUTPUT"    

THE GLOBAL OLEORESIN MARKET IS CONCENTRATED IN NATURE WITH FEWER COMPANIES HOLDING A MAJOR SHARE IN THE INDUSTRY. THE GLOBAL INDUSTRY IS EXPECTED TO WITNESS AN INCREASE IN MERGERS, ACQUISITIONS AND STRATEGIC ALLIANCES OVER THE NEXT SEVEN YEARS.    

MAJOR COMPANIES INCLUDE UNIVERSAL OLEORESINS, UNGERER & COMPANY,

PLANT LIPIDS, AKAY, SYNTHITE, AVT NATURAL PRODUCTS LTD, INDO WORLD,
  PAPRIKA OLEO’S, PARAS PERFUMERS, AMBE GROUP, ASIAN OLEORESIN
  COMPANY, CYMBIO PHARMA PVT LTD AND BIOPREX LABS.    

OLEORESIN MARKET KEY DEVELOPMENTS    

OLEORESIN MARKET MAJOR PLAYERS    

EUROPE AN INTERESTING MARKET FOR OLEORESINS    

EUROPEAN INDUSTRY INCREASINGLY USES FORMULAS WITH NATURAL
   INGREDIENTS    

ETHNIC FOODS ARE GAINING POPULARITY    

SALT REDUCTION PROVES TO BE A CHALLENGE    

REQUIREMENTS MUST OLEORESINS COMPLY WITH TO BE ALLOWED
   ON THE EUROPEAN MARKET    

QUALITY REQUIREMENTS    

COLOUR AND FLAVOR    

PURITY    

INDIA DOMINATES THE OLEORESIN MARKET    

BUYERS SHOW INTEREST IN NATURAL SUBSTITUTES    

NEED FOR PRODUCT DISTINCTION    

TWO MARKET SEGMENTS FOR OLEORESINS    

TARGET IMPORTERS    

EXPORTS TO FLAVOURING MANUFACTURERS    

END-MARKET PRICES FOR OLEORESINS    

VALUE ADDITION BY IMPORTERS    

PRICE DEVELOPMENTS FOR SELECTED OLEORESINS, FOURTH QUARTER 2017    

LABELLING & PACKAGING REQUIREMENTS    

LABELLING    

YOUR LABELS MUST INCLUDE    

PACKAGING    

PLANT & MACHINERY MANUFACTURER    

CHILLI SUPPLIERS    

RAW MATERIAL PHOTOGRAPHS    

PRODUCT PHOTOGRAPHS    

MACHINERY PHOTOGRAPHS    

PRESSURE REGULATING EQUIPMENT    

TRIPLEX PLUNGER PUMPS MAX. FLOW RATE OF 600 LTR/HR    

CO2 PRESSURE INCREASE FROM 50 BAR TO 300 BAR    

CO2 PASSED THROGH SUPER HEATER TO REACH A SUPER CRITICAL STATE    

FOOD GRADE STAINLESS STEEL 316/304    

SEPARATION OF UTILITY AREA AND CLEQN AREA EQUIPMENT    

SCADA SYSTEM WITH ABILITY ADD NEW RECIPES    

ACTIVE SYSTEM MONITORING FOR SAFETY AND RELIABILITY USING PRESSSURE GAUGES, PRESSURE TRANDUCERS    

ADVANCED INTEGRATED CONTROLS AND COMMUNICATION    

SPECIALLY DESIGNED HEAT EXCENGER TO OPTIMIZE DESIGN TEMPERATURE    

THE CO2 IN SUPER CRITICAL STATE PASSES THROUGH THE EXTYRACTOR
   AND CARRIES WIT IT THE ESSENTIAL OILS AND NATURAL EXTRACTS.    

THE CO2 IN THE SEPARATPOR AT LOWER PRESSURE TURNS IN TO A GAS AND THE EXTRACT IS SEPARATED DUE TO THE GAS LIQUID SEPARATION.    


    
APPENDIX – A:

01.    PLANT ECONOMICS    
02.    LAND & BUILDING     
03.    PLANT AND MACHINERY    
04.    OTHER FIXED ASSESTS    
05.    FIXED CAPITAL    
06.    RAW MATERIAL    
07.    SALARY AND WAGES    
08.    UTILITIES AND OVERHEADS    
09.    TOTAL WORKING CAPITAL    
10.    TOTAL CAPITAL INVESTMENT    
11.    COST OF PRODUCTION    
12.    TURN OVER/ANNUM    
13.    BREAK EVEN POINT     
14.    RESOURCES FOR FINANCE    
15.    INSTALMENT PAYABLE IN 5 YEARS    
16.    DEPRECIATION CHART FOR 5 YEARS    
17.    PROFIT ANALYSIS FOR 5 YEARS    
18.    PROJECTED BALANCE SHEET FOR (5 YEARS)